THE EFFECT OF INTRAPARTICLE DIFFUSION ON CATALYTIC PROCESSES IN A FLUIDIZED-BED REACTOR WITH DECAYING CATALYST - INTRAPARTICLE DIFFUSION INFLUENCES ONLY CATALYTIC REACTIONS

被引:0
作者
GRZESIK, M
SKRZYPEK, J
WOJCIECHOWSKI, BW
机构
[1] KRAKOW TECH UNIV,INST IND EQUIPMENT & POWER ENGN,PL-31155 KRAKOW,POLAND
[2] QUEENS UNIV,DEPT CHEM ENGN,KINGSTON K7L 3N6,ONTARIO,CANADA
[3] POLISH ACAD SCI,INST CHEM ENGN,GLIWICE,POLAND
来源
INZYNIERIA CHEMICZNA I PROCESOWA | 1992年 / 13卷 / 01期
关键词
D O I
暂无
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
The effect of intraparticle diffusion on catalytic processes in a fluidized-bed reactor with decaying catalyst was analysed in detail assuming that the inteRNal mass transport can influence only catalytic reactions. It was found that for the fluidized-bed reactor modelled as CSTR (with no fresh catalyst feed) the change in internal resistance of the mass transport does not affect the existence of three deactivation classes as defined by Wojciechowski. Furthermore, it was shown that in the fluidized-bed reactor with a continuous fresh catalyst feed, each level of internal diffusion resistance corresponds to different selectivity curve and the increase in deactivation rate may cause the increase in selectivity of complex reactions.
引用
收藏
页码:131 / 153
页数:23
相关论文
共 50 条
  • [41] ANALYSIS OF VOLUME CHANGE EFFECTS IN A FLUIDIZED-BED CATALYTIC REACTOR
    SHIAU, CY
    LIN, CJ
    JOURNAL OF CHEMICAL TECHNOLOGY AND BIOTECHNOLOGY, 1993, 56 (03) : 295 - 303
  • [42] Catalytic oxidation of methanol to formaldehyde in a continuous fluidized-bed reactor
    Sohrabi, M
    Aghdasinia, H
    CHEMICAL ENGINEERING & TECHNOLOGY, 2003, 26 (01) : 69 - 73
  • [43] A REVISED MODEL FOR PREDICTING THE PERFORMANCE OF A FLUIDIZED-BED CATALYTIC REACTOR
    PEREIRA, J
    CHANDRASEKHARAN, K
    CALDERBANK, PH
    CHEMICAL ENGINEERING SCIENCE, 1981, 36 (02) : 239 - 242
  • [44] Ultrasound assisted catalytic wet peroxide oxidation of phenol: kinetics and intraparticle diffusion effects
    Nikolopoulos, AN
    Igglessi-Markopoulou, O
    Papayannakos, N
    ULTRASONICS SONOCHEMISTRY, 2006, 13 (01) : 92 - 97
  • [45] Tracking Catalyst Activity during Fluidized-bed Catalytic Cracking
    Jimenez-Garcia, Gladys
    Aguilar-Lopez, Ricardo
    Leon-Becerril, Elizabeth
    Maya-Yescas, Rafael
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2009, 48 (03) : 1220 - 1227
  • [46] A model for catalytic synthesis of carbon nanotubes in a fluidized-bed reactor: Effect of reaction heat
    Rabinovich, Oscar
    Tsytsenka , Alla
    Kuznetsov, Vladimir
    Moseenkov, Sergei
    Krasnikov, Dmitry
    CHEMICAL ENGINEERING JOURNAL, 2017, 329 : 305 - 311
  • [47] EFFECT OF INTRAPARTICLE DIFFUSION ON THE DETERMINATION OF THE GAS-LIQUID VOLUMETRIC OXYGEN-TRANSFER COEFFICIENT IN A 3-PHASE FLUIDIZED-BED CONTAINING POROUS PARTICLES
    SUN, Y
    FURUSAKI, S
    JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 1989, 22 (05) : 556 - 559
  • [48] Catalytic upgrade for pyrolysis of food waste in a bubbling fluidized-bed reactor
    Hoang Vu Ly
    Quoc Khanh Tran
    Kim, Seung-Soo
    Kim, Jinsoo
    Choi, Suk Soon
    Oh, Changho
    ENVIRONMENTAL POLLUTION, 2021, 275
  • [49] THE FLUIDIZED-BED CATALYTIC REACTOR - A LEARNING-MODEL FOR FAST REACTION
    PIGEON, RG
    CARBERRY, JJ
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 1990, 29 (06) : 1013 - 1019
  • [50] CATALYTIC-OXIDATION OF FORMIC-ACID IN WATER - INTRAPARTICLE DIFFUSION IN LIQUID-FILLED PORES
    BALDI, G
    GOTO, S
    CHOW, CK
    SMITH, JM
    INDUSTRIAL & ENGINEERING CHEMISTRY PROCESS DESIGN AND DEVELOPMENT, 1974, 13 (04): : 447 - 452